EP1252179B1 - Lipopeptides a haute purete, micelles de lipopeptides et procedes de preparation - Google Patents

Lipopeptides a haute purete, micelles de lipopeptides et procedes de preparation Download PDF

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Publication number
EP1252179B1
EP1252179B1 EP01903121A EP01903121A EP1252179B1 EP 1252179 B1 EP1252179 B1 EP 1252179B1 EP 01903121 A EP01903121 A EP 01903121A EP 01903121 A EP01903121 A EP 01903121A EP 1252179 B1 EP1252179 B1 EP 1252179B1
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Prior art keywords
daptomycin
lipopeptide
anion exchange
preferred
purified
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German (de)
English (en)
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EP1252179A2 (fr
Inventor
Thomas J. Kelleher
Jan-Ji Lai
Joseph P. Decourcey
Paul D. Lynch
Maurizio Zenoni
Auro R. Tagliani
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Cubist Pharmaceuticals LLC
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Cubist Pharmaceuticals LLC
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Priority to EP09014616A priority Critical patent/EP2159229A1/fr
Priority to EP15173312.8A priority patent/EP2940034B1/fr
Priority to EP05015374A priority patent/EP1586580B1/fr
Priority to DK05015374.1T priority patent/DK1586580T3/da
Priority to EP10174862.2A priority patent/EP2264047B1/fr
Application filed by Cubist Pharmaceuticals LLC filed Critical Cubist Pharmaceuticals LLC
Priority to EP15173324.3A priority patent/EP2940036B1/fr
Publication of EP1252179A2 publication Critical patent/EP1252179A2/fr
Publication of EP1252179B1 publication Critical patent/EP1252179B1/fr
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Priority to CY20151100831T priority patent/CY1116827T1/el
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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14—Extraction; Separation; Purification
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K38/00—Medicinal preparations containing peptides
    • A61K38/04—Peptides having up to 20 amino acids in a fully defined sequence; Derivatives thereof
    • A61K38/12—Cyclic peptides, e.g. bacitracins; Polymyxins; Gramicidins S, C; Tyrocidins A, B or C
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K38/00—Medicinal preparations containing peptides
    • A61K38/04—Peptides having up to 20 amino acids in a fully defined sequence; Derivatives thereof
    • A61K38/10—Peptides having 12 to 20 amino acids
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P29/00—Non-central analgesic, antipyretic or antiinflammatory agents, e.g. antirheumatic agents; Non-steroidal antiinflammatory drugs [NSAID]
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P31/00—Antiinfectives, i.e. antibiotics, antiseptics, chemotherapeutics
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P31/00—Antiinfectives, i.e. antibiotics, antiseptics, chemotherapeutics
    • A61P31/04—Antibacterial agents
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P31/00—Antiinfectives, i.e. antibiotics, antiseptics, chemotherapeutics
    • A61P31/10—Antimycotics
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14—Extraction; Separation; Purification
    • C07K1/145—Extraction; Separation; Purification by extraction or solubilisation
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14—Extraction; Separation; Purification
    • C07K1/16—Extraction; Separation; Purification by chromatography
    • C07K1/18—Ion-exchange chromatography
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
    • C07K1/14—Extraction; Separation; Purification
    • C07K1/16—Extraction; Separation; Purification by chromatography
    • C07K1/20—Partition-, reverse-phase or hydrophobic interaction chromatography
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K5/00—Peptides containing up to four amino acids in a fully defined sequence; Derivatives thereof
    • C07K5/04—Peptides containing up to four amino acids in a fully defined sequence; Derivatives thereof containing only normal peptide links
    • C07K5/08—Tripeptides
    • C07K5/0821—Tripeptides with the first amino acid being heterocyclic, e.g. His, Pro, Trp
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K7/00—Peptides having 5 to 20 amino acids in a fully defined sequence; Derivatives thereof
    • C07K7/04—Linear peptides containing only normal peptide links
    • C07K7/08—Linear peptides containing only normal peptide links having 12 to 20 amino acids
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K7/00—Peptides having 5 to 20 amino acids in a fully defined sequence; Derivatives thereof
    • C07K7/64—Cyclic peptides containing only normal peptide links
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P21/00—Preparation of peptides or proteins
    • C12P21/02—Preparation of peptides or proteins having a known sequence of two or more amino acids, e.g. glutathione
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S435/00—Chemistry: molecular biology and microbiology
    • Y10S435/8215—Microorganisms
    • Y10S435/822—Microorganisms using bacteria or actinomycetales
    • Y10S435/886—Streptomyces

Definitions

  • the present invention relates to a process for preparing the highly purified form of the lipopeptide daptomycin.
  • the present invention further relates to micelles of the lipopeptide.
  • the present invention also relates to methods of making the lipopeptide micelles from non-associated monomers of the lipopeptides, and for converting lipopeptide micelles to non-associated monomers.
  • the present invention also relates to a process for preparing lipopeptides using micelles that is easily scaled for commercial production.
  • Dptomycin has potent bactericidal activity in vitro against clinically relevant gram-positive bacteria that cause serious and life-threatening diseases.
  • These bacteria include resistant pathogens, such as vancomycin-resistant enterococci (VRE), methicillin-resistant Staphylococcus aureus (MRSA), glycopeptide intermediary susceptible Staphylococcus aureus (GISA), coagulase-negative staphylococci (CNS), and penicillin-resistant Streptococcus pneumoniae (PRSP), for which there are very few therapeutic alternatives.
  • VRE vancomycin-resistant enterococci
  • MRSA methicillin-resistant Staphylococcus aureus
  • GISA glycopeptide intermediary susceptible Staphylococcus aureus
  • CNS coagulase-negative staphylococci
  • PRSP penicillin-resistant Streptococcus pneumoniae
  • Daptomycin's inhibitory effect is a rapid, concentration-dependent bactericidal effect in vitro and in vivo, and a relatively prolonged concentration-dependent post-antibiotic effect in vivo.
  • Daptomycin is described by Baltz in Biotechnology of Antibiotics. 2nd Ed. , ed. W.R. Strohl (New York: Marcel Dekker, Inc.), 1997, pp. 415-435, hereafter "Baltz.”
  • Daptomycin also known as LY 146032, is a cyclic lipopeptide antibiotic that can be derived from the fermentation of Streptomyces roseosporus.
  • Daptomycin is a member of the factor A-21978C 0 type antibiotics of S . roseosporus and is comprised of a decanoyl side chain linked to the N-terminal tryptophan of a cyclic 13-amino acid peptide (Fig. 1).
  • Daptomycin has an excellent profile of activity because it is highly effective against most gram-positive bacteria; it is highly bactericidal and fast-acting; it has a low resistance rate and is effective against antibiotic-resistant organisms.
  • the compound is currently being developed in a variety of formulations to treat serious infections caused by bacteria, including, but not limited to, methicillin resistant Staphylococcus aureus (MRSA) and vancomycin resistant enterococci (VRE).
  • MRSA methicillin resistant Staphylococcus aureus
  • VRE vancomycin resistant enterococci
  • a number of United States Patents describe A-21978C antibiotics and derivatives thereof including daptomycin (LY 146032) as well as methods of producing and isolating the A-21978C antibiotics and derivatives thereof.
  • United States Patent Re. 32,333, Re. 32,455 and 4,800,157 describe a method of synthesizing daptomycin by cultivating Streptomyces roseosporus NRL 15998 under submerged aerobic fermentation conditions.
  • United States Patent 4,885,243 describes an improved method of synthesizing daptomycin by feeding a fermentation culture a decanoic fatty acid or ester or salt thereof.
  • United States Patents Re. 32,310, Re. 32,311, 4,537,717, 4,482,487 and 4,524,135 describe methods of deacylating the A-21978C antibiotic and reacylating the peptide nucleus and antibiotic derivatives made by this process. All of these patents describe a purified deacylated A-21978C antibiotic nucleus or a derivative thereof which was isolated from the fermentation broth by filtration and then purified by Diaion HP-20 chromatography and silica gel/C18 chromatography.
  • United States Patents Re. 32,333 and Re. 32,455 disclose a purification method in which a filtrate of whole fermentation broth was purified through a number of precipitation and extraction steps to obtain a crude A-21978C complex.
  • the crude complex was further purified by ion exchange chromatography on IRA-68 and two rounds of silica gel chromatography. Individual A-21978C factors were separated by reverse-phase silica gel or silica gel/C18.
  • United States Patents Re. 32,333 and Re. 32,455 also disclose that A-21978C may be purified by batch chromatography using Diaion HP-20 resin followed by silica-gel column chromatography.
  • United States Patent 4,874,843 describes a daptomycin purification method in which the fermentation broth was filtered and passed through a column containing HP-20 resin. After elution, the semipurified daptomycin was passed through a column containing HP-20ss, and then separated again on HP-20 resin.
  • the '843 patent states that final resolution and separation of daptomycin from structurally similar compounds by this method is impeded by the presence of impurities that are not identifiable by ultraviolet analysis of the fermentation broth.
  • the '843 patent further states that attempts to remove these impurities by reverse phase chromatography over silica gel, normal phase chromatography over silica gel or ion exchange chromatography also failed to significantly improve the purity of daptomycin.
  • the '843 patent also discloses a "reverse method" for purification comprising the steps of contacting an aqueous solution of the fermentation product with a non-functional resin in aqueous phase, physically removing the water from the charged resin, rewetting the charged resin with a polar organic solvent, washing the resin with the organic solvent, eluting the fermentation product from the resin by increasing the polarity of the solvent and recovering the fermentation product.
  • This method improves the final purity from about 80% to about 93% and increases the yield from about 5% to about 35%; however, the '843 patent does not disclose the type of impurities present in the daptomycin preparation.
  • United States Patent 5,912,226 describes the identification and isolation of two impurities produced during the manufacture of daptomycin. Daptomycin, an ⁇ -aspartyl peptide, becomes transpeptidated to form a stable intermediate in which the aspartyl group becomes an anhydro-succinimido group (Fig. 3). The '226 patent teaches that the presence of this intermediate, designated anhydro-daptomycin, is more pronounced at pH 4-6. Rehydration of the anhydro-succinimido form produces a second degradation product that contains an ⁇ -aspartyl group and is designated the ⁇ -isomer form of daptomycin (Fig. 2).
  • the '226 patent discloses that the t-BOC derivative of anhydro-daptomycin may be isolated by chromatography over reverse phase silica gel/C-18 column, precipitated, and repurified by reverse phase silica gel/C-18 chromatography.
  • the '226 patent also teaches that the ⁇ -isomer form of daptomycin may be purified by chromatography over a Diaion HP-20ss resin. desalted by chromatography over a Diaion HP-20 resin, and further purified using a reverse-phase C-18 column followed by a HP-20 resin column in reverse mode.
  • Kirsch et. al. (Pharmaceutical Research, 6:387-393, 1989, hereafter "Kirsch") stated that anhydro-daptomycin and the ⁇ -isomer were produced in the purification of daptomycin. Kirsch described methods to minimize the levels of anhydro-daptomycin and the ⁇ -isomer through manipulation of pH conditions and temperature conditions. However, Kirsch was unable to stabilize daptomycin and prevent the conversion of daptomycin to anhydro-daptomycin and its subsequent isomerization to ⁇ -isomer. Kirsch was also unable to prevent the degradation of daptomycin into other degradation products unrelated to anhydro-daptomycin and ⁇ -isomer.
  • daptomycin may be prepared using these procedures so that the daptomycin contains no more than 2.5% by weight of a combined total of anhydro-daptomycin and ⁇ -isomer, but gives no indication of the levels of other impurities.
  • the highest daptomycin purity levels observed has been about 90%-93%.
  • the instant invention addresses these problems by providing commercially feasible methods to produce high levels of purified the lipopeptide dapthomycin.
  • commercially feasible methods are disclosed that results in daptomycin at a purity level of 95-97%.
  • a commercially feasible method is disclosed that almost completely eliminates the major impurities anhydro-daptomycin and ⁇ -isomer as well as other impurities in preparations of daptomycin.
  • separating lipopeptide micelles from low molecular weight contaminants and separating non-associated lipopeptides from high molecular weight contaminants comprising separating lipopeptide micelles from low molecular weight contaminants and separating non-associated lipopeptides from high molecular weight contaminants.
  • HPLC high performance liquid chromatography
  • the invention also provides purified daptomycin that possesses a purity of at least 98% or that is substantially or essentially free of anhydro-daptomycin and ⁇ -isomer.
  • the invention provides purified daptomycin that is free or essentially free of anhydro-daptomycin and contains a much lower level of the ⁇ -isomer and of other contaminants than was previously possible to obtain in the prior art.
  • the invention also provides lipopeptide micelles.
  • the micelle comprises daptomycin or a daptomycin-related lipopeptide.
  • the invention also provides pharmaceutical compositions comprising highly purified daptomycin or a daptomycin-related lipopeptide micelles and methods of using these compositions.
  • One object of the present invention is to provide a method for purifying lipopeptides that is easily scaled for commercial production comprising a unique combination of anion exchange chromatography and hydrophobic interaction chromatography.
  • the method is used to manufacture purified daptomycin that is greater than 95% pure and exhibits reduced levels of impurities compared to daptomycin prepared by prior art methods.
  • the method is used to manufacture daptomycin using reduced levels of solvents compared to those used in prior art methods.
  • the method is used to manufacture purified daptomycin-related lipopeptides that are greater than 95% pure.
  • Another object of the present invention is to provide a method for increasing the levels of a lipopeptide produced by a microorganism by feeding the fermentation culture a reduced level of a fatty acid.
  • Using lower levels of decanoic acid than those proposed for daptomycin fermentation in United States Patent 4,885,243 results in improved economics in addition to producing a highly pure form of daptomycin or a daptomycin-related lipopeptide.
  • the method is used to increase the concentration and amount of daptomycin produced by Streptomyces roseosporus while minimizing the production of related contaminants. Lower levels of contaminants in the fermentation broth results in a more efficient recovery and purification of daptomycin, which provides for a manufacturing process with a higher yield.
  • Another object of the present invention is to provide a method for purifying daptomycin or daptomycin related lipopeptides comprising the use of modified buffer enhanced anion exchange chromatography.
  • the method is used to produce daptomycin that is at least 98% pure or that is substantially or essentially free of anhydro-daptomycin or ⁇ -isomer.
  • the method is used to purify daptomycin-related lipopeptides to at least 98% purity.
  • Another object of the present invention is to provide a process chromatography method to purify the lipopeptide dapthomycin comprising a novel combination of anion exchange chromatography, hydrophobic interaction chromatography and modified buffer enhanced anion exchange chromatography.
  • the process chromatography method is used to purify daptomycin or a daptomycin-related lipopeptide.
  • the modified buffer unexpectedly permits a separation of anhydro-daptomycin from daptomycin not previously possible in prior chromatography methods.
  • Another object of the invention is to provide a method for purifying the lipopeptide dapthomycin that is easily scaled for commercial production using lipopeptide micelles.
  • the method comprises converting a lipopeptide solution from a monomeric, nonmicellar state to a micellar state and back again during purification procedures.
  • the method comprises subjecting the lipopeptide to conditions in which micelles are formed, separating the lipopeptide micelles from low molecular weight contaminants by, e.g., a size separation technique.
  • the method comprises subjecting the lipopeptides to conditions in which the lipopeptides are in monomeric form and separating the monomeric lipopeptide molecules from high molecular weight molecules or aggregates by, e.g., a size separation technique.
  • the method comprises both steps: subjecting the lipopeptides to conditions in which micelles are formed and separating the lipopeptide micelles from low molecular weight contaminants, and then subjecting the lipopeptide micelles to conditions in which the lipopeptides are in monomeric form and separating the lipopeptide monomers from high molecular weight molecules or aggregates. These two steps may be performed in either order.
  • the size separation technique is ultrafiltration or size exclusion chromatography.
  • a further object of the present invention is to provide improved methods for measuring the purity of the lipopeptide, daptomycin, by high pressure liquid chromatography (HPLC).
  • Another object of the present invention is to provide purified the lipopeptide daptomycin or a daptomycin-related lipopeptide, and pharmaceutically acceptable salts or formulations thereof.
  • the present invention provides daptomycin or a daptomycin-related lipopeptide purified by one of the methods described in the specification.
  • Another object of the present invention is to provide lipopeptide micelles and pharmaceutically acceptable formulations thereof.
  • the present invention provides daptomycin micelles or a daptomycin-related lipopeptide micelle and pharmaceutically acceptable formulations thereof.
  • the invention also provides methods of administering the lipopeptide micelles or pharmaceutical formulations thereof to patients in need thereof.
  • the lipopeptide micelles are administered intravenously, parenterally, intramuscularly or topically.
  • isolated refers to a compound or product that is refers to a compound which represents at least 10%, preferably at least 20% or 30%, more preferably at least 50%, 60% or 70%, and most preferably at least 80% or 90% of the compound present in the mixture.
  • lipopeptide refers to a dapthomycin or related molecule, as well as salts, esters, amides and ethers thereof.
  • lipopeptide also encompasses protected forms of lipopeptides in which one or more amino, carboxylate or hydroxyl groups are protected. See, e.g., "Protective Groups in Organic Synthesis” by Theodora W. Greene, John Wiley and Sons, New York, 1981 for examples of protecting groups.
  • the lipopeptide is an antibiotic.
  • the lipopeptide is LY 303366, echinocandins, pneumocandias, aculeacins, surfactin, plipastatin B1, amphomycin or the lipopeptide derivative disclosed in United States Patent 5,629,288.
  • these lipopeptides are known in the art. See, e.g., United States Patent 5,202,309 and International PCT Application WO 00/08197.
  • the lipopeptide is a daptomycin-related molecule, including, inter alia, daptomycin, A54145, a daptomycin-related lipopeptide disclosed in United States Patent 4,537,717, 4,482,487, Re. 32,311, Re.
  • the daptomycin-related lipopeptides disclosed in 60/170,943, 60/170,946, 60/170,945, and 60/208,222 relate to synthetic and semisynthetic lipopeptides in which the ornithine or kynurine residues or the fatty acid side chain of daptomycin are modified.
  • the lipopeptide is daptomycin.
  • daptomycin-related lipopeptide refers to compounds described above, and salts thereof.
  • daptomycin refers to the n-decanoyl derivative of the factor A-21978C 0 type antibiotic, or a pharmaceutical acceptable salt thereof. "Daptomycin” is synonymous with LY146032. See Fig. 1.
  • anhydro-daptomycin refers to the daptomycin derivative in which the ⁇ -aspartyl group of daptomycin is transpeptidated to an anhydro-succinimido group. See Fig. 3.
  • ⁇ -isomer or " ⁇ -isomer of daptomycin” refers to the daptomycin derivative that contains a ⁇ -aspartyl group instead of an ⁇ -aspartyl group. See Fig. 2.
  • Daptomycin or a daptomycin-related lipopeptide is "substantially pure” when at least 95% of a sample is daptomycin or daptomycin-related lipopeptide.
  • daptomycin or daptomycin-related lipopeptide is “substantially pure” when at least 97% of a sample is daptomycin or daptomycin-related lipopeptide.
  • Daptomycin or daptomycin-related lipopeptide is "essentially pure” when at least 98% of a sample is daptomycin or daptomycin-related lipopeptide.
  • daptomycin or daptomycin-related lipopeptide is "essentially pure” when at least 99% of a sample is daptomycin or daptomycin-related lipopeptide.
  • Daptomycin or daptomycin-related lipopeptide is "substantially free" of another compound when the other compound is present in an amount that is no more than 1% of the amount of the daptomycin or daptomycin-related lipopeptide preparation.
  • Daptomycin or daptomycin-related lipopeptide is "essentially free" of another compound when the other compound is present in an amount that is no more than 0.5% of the amount of the daptomycin or daptomycin-related lipopeptide preparation.
  • Daptomycin or daptomycin-related lipopeptide is “free” of another compound when the other compound is present in an amount that is no more than 0.1% of the amount of the daptomycin or daptomycin-related lipopeptide preparation.
  • daptomycin or daptomycin-related lipopeptide is "free” of another compound when the compound cannot be detected by HPLC under conditions of maximum sensitivity in which a limit of detection is approximately 0.05% or less of the amount of the daptomycin or daptomycin-related lipopeptide preparation.
  • Exemplary HPLC methods are described herein (Tables 1 and 2).
  • “Purified” daptomycin or daptomycin-related lipopeptide refers to substantially pure daptomycin or daptomycin-related lipopeptide, essentially pure daptomycin or daptomycin-related lipopeptide, or a salt thereof, or to daptomycin, daptomycin-related lipopeptide, or a salt thereof which is substantially free, essentially free, or free of another compound.
  • Partially purified daptomycin or daptomycin-related lipopeptide refers to daptomycin, daptomycin-related lipopeptide, or a salt thereof that is less than 90% pure.
  • the purity of daptomycin, daptomycin-related lipopeptide or of another lipopeptide refers to the lipopeptide prior to its formulation in a pharmaceutical composition.
  • the purity may be measured by any means including nuclear magnetic resonance (NMR), gas chromatography/mass spectroscopy (GC/MS), liquid chromatography/mass spectroscopy (LC/MS) or microbiological assays.
  • NMR nuclear magnetic resonance
  • GC/MS gas chromatography/mass spectroscopy
  • LC/MS liquid chromatography/mass spectroscopy
  • HPLC high pressure liquid chromatography
  • micelle refers to aggregates of amphipathic molecules. In an aqueous media, the lipophilic domains of the molecules of the aggregate are oriented toward the interior of the micelle and the hydrophilic domains are in contact with the medium.
  • Micelle structures include, but are not limited to, spherical, laminar, cylindrical, ellipsoidal, vesicular (liposomal), lamellar and liquid crystal. See Fig. 14.
  • mixed micelle refers to a particular type of micelle in which the micelle contains more than a single type of amphipathic molecule.
  • mixed micelles contain a lipopeptide and at least one other amphipathic molecule which may be another lipopeptide.
  • Mixed micelles contain at least 10% of the lipopeptide by weight. In other embodiments, a mixed micelle contains at least 20%, 30%, 40%, 50%, 60%, 70%, 80% or 90% of the lipopeptide.
  • mice solution refers to a solution in which more than 50% of the lipopeptide molecules in the solution are present in micelles, as measured by weight. Preferably, at least 60%, 70%, 80%, 90% or 95% of the molecules are present in micelles. A micellar solution is retained on a ultrafiltration membrane that has a 10,000 dalton nominal molecular weight (NMW) cutoff.
  • NMW nominal molecular weight
  • cmc critical micelle concentration
  • monomer refers to an amphipathic molecule that is not part of an aggregate but that exists as a single molecule.
  • the term monomer refers to a non-associated lipopeptide.
  • monomeric solution refers to a solution in which more than 50% of the lipopeptide molecules are present as monomers as measured by weight. Preferably at least 60%, 70%, 80%, 90% or 95% are present as monomers. A monomeric solution is not retained on a ultrafiltration membrane that has a 10,000 dalton NMW cutoff but rather passes through the membrane.
  • low ionic strength buffer refers to a solution that has a salt concentration below 50mM
  • medium ionic strength buffer refers to a solution that has a salt concentration between 50-250mM
  • high ionic strength buffer refers to a solution that has a salt concentration greater than 250mM.
  • One embodiment of the present invention is drawn to a process chromatography method that produces a purified lipopeptide in a commercially feasible manner, wherein the lipopeptide is daptomycin or a daptomycin-related lipopeptide.
  • the process chromatography method comprises sequentially using anion exchange chromatography, hydrophobic interaction chromatography (HIC) and anion exchange chromatography to purify a preparation containing a lipopeptide, such as daptomycin or a daptomycin-related lipopeptide.
  • HIC hydrophobic interaction chromatography
  • the purification method further comprises altering the fermentation conditions in which the A21978C-containing crude product is produced by Streptomyces roseosporus in order to increase daptomycin production and decrease impurities and related contaminants produced by the S . roseosporus fermentation culture.
  • the extracellular solution is clarified by removing the mycelia from the fermentation broth. Removing the mycelia from the fermentation is performed by any standard separation technique, such as centrifugation or microfiltration.
  • the fermentation broth is clarified by microfiltration, such as by using a Pall SepTM membrane system.
  • the fermentation broth is clarified using an industrial centrifuge, such as a WestfaliaTM centrifuge, followed by a finishing depth filter.
  • Other devices such as filter presses, rotary drum filters or disposable depth filters, may be used to remove mycelia from fermentation broth to produce a clarified broth suitable for large-scale column chromatography.
  • daptomycin may be extracted from mycelial fermentation directly by using an organic solvent such as butanol prior to clarification on a solvent separating centrifuge or filter. Any alcohol with four carbons or more may be used in the extraction according to this embodiment.
  • a preferred solvent is n-butanol.
  • Using an organic solvent results in an initial additional purification of daptomycin compared to a purely aqueous separation of daptomycin. For example, daptomycin partitions into n-butanol when n-butanol is used in a concentration greater than 10% and when the process is conducted under conditions in which the n-butanol forms a separate phase, e . g ., at a pH value of 4-5, which is near the isoelectric point of daptomycin (see Example 4).
  • daptomycin is produced in an immobilized reactor that uses preactivated mycelia for the non-fermentation production of daptomycin using an energy source, preferably a sugar, elemental components, such as amino acids and ammonia, and decanoic acid. Production of daptomycin in an immobilized enzyme reactor is then processed by methods described herein.
  • an energy source preferably a sugar, elemental components, such as amino acids and ammonia, and decanoic acid.
  • the levels of daptomycin are enriched, ( i . e . concentrated) in the clarified solution by anion exchange chromatography.
  • the clarified solution is first contacted with an anion exchange resin under conditions in which most or all of daptomycin binds to the anion exchange resin. After binding, the resin is washed with an appropriate ionic aqueous buffer to remove unbound material and some of the daptomycin impurities. Finally, the purified daptomycin bound to the resin is eluted under conditions in which daptomycin will dissociate from the resin.
  • the binding, washing and elution steps may be performed according to this invention using buffers and methods known in the art.
  • elution may be performed by using a buffer containing an elevated salt concentration compared to the wash buffer, a buffer that has a lower pH compared to the wash buffer, or a buffer that has both a higher salt concentration and a lower pH than the wash buffer.
  • daptomycin is bound to the anion exchange resin that has been equilibrated in a buffer containing no added salt or a low salt concentration at a pH that is neutral to basic.
  • the loaded resin is washed with three column bed volumes of water and then three to six bed volumes of an intermediate salt buffer containing 30 to 60 mM NaCl.
  • Daptomycin is eluted from the column with one to three column volumes of an elevated salt and/or lower pH buffer containing 300 to 500 mM NaCl. Higher concentrations of sodium chloride and alternative salts such as potassium chloride will also elute daptomycin from the resin.
  • a high flow rate anionic exchange resin is used.
  • FP-DA 13 resin (Mitsubishi) is used.
  • the anion exchange chromatography may be performed by column chromatography or may be accomplished in batch mode. For commercial production, it may be preferred to use batch mode.
  • the anion exchange resin may be washed and eluted with stepwise salt gradients or with a continuous salt gradient.
  • a suitable stepwise or continuous salt gradient is any one that permits the separation of daptomycin from contaminants.
  • a continuous salt gradient is one which ranges from 0 to 1000 mM NaCl.
  • a continuous salt gradient is one which ranges from 100 to 500 mM NaCl or from 0 to 400 mM NaCl.
  • Radial flow chromatography may also be used, as described in United States Patents 5,756,680, 4,865,729, 4,840,730 or 4,708,782.
  • the daptomycin preparation is further purified by hydrophobic interaction chromatography (HIC).
  • HIC hydrophobic interaction chromatography
  • the eluted aqueous daptomycin preparation is contacted with a HIC resin under conditions in which most or all of daptomycin will bind to the resin.
  • the water content of the daptomycin-loaded resin is reduced by contacting the resin with an increased concentration of a non-polar solvent.
  • the resin is washed with an appropriate polar organic solvent under conditions in which impurities dissociate from the resin while daptomycin remains bound.
  • the daptomycin preparation is eluted under conditions in which daptomycin dissociates from the resin.
  • daptomycin is eluted using a solvent-containing buffer with a lower polarity (higher polar solvent level) and/or higher pH than the wash buffer.
  • the non-functional resin for HIC is small particle HP-20ss (Mitsubishi).
  • the bound daptomycin is specifically removed from the HP-20ss resin with an organic phase solvent, such as one containing isopropyl alcohol, acetonitrile, butanol or other suitable solvent.
  • daptomycin is bound to HP-20ss resin that has been equilibrated in an acetate buffer containing 10% acetonitrile or equivalent polar solvent, such as isopropyl alcohol.
  • the daptomycin-loaded resin is washed with at least three column bed volumes of equilibration buffer.
  • the daptomycin-loaded resin is further freed of additional impurities by washing with three to six bed volumes of an acetate wash buffer containing a non-eluting concentration of the polar solvent.
  • the daptomycin-loaded resin is washed with 30% acetonitrile or 45% isopropyl alcohol.
  • the daptomycin-loaded resin is eluted with one to three bed volumes of acetate buffer containing 35% or more acetonitrile or greater than 50% isopropyl alcohol.
  • daptomycin is eluted with 35% acetonitrile at pH 4.0-5.0 or 55-60% isopropyl alcohol.
  • the daptomycin-loaded resin is eluted with one to three bed volumes of buffer at an increased pH.
  • the pH of the buffer is gradually increased to elute different compounds from the column at different rates due to charge differences.
  • the elution concentration of acetonitrile is reduced to 10-20%.
  • the elution concentration of isopropyl alcohol is reduced to 20-25%.
  • Control of the temperature under which chromatography is performed also influences solvent concentration. Elution at lower temperatures, i.e., under refrigerated conditions, requires increased levels of solvent at all pH conditions.
  • the organic solvent in the daptomycin preparation is reduced by anion exchange chromatography.
  • FP-DA 13 is used as discussed supra.
  • the purified daptomycin is depyrogenated, filtered and concentrated under refrigerated conditions.
  • Filtering daptomycin may be performed by any method known in the art. In one embodiment, filtering and depyrogenating may be performed by:
  • daptomycin of step (ii) is filtered under pressure on a 10,000 dalton molecular weight cutoff (MWCO) ultra-filter at a pH of approximately 7-8.
  • daptomycin is at an initial concentration of less than 40 mg/ml, more preferably, at a concentration of approximately 31.25 mg/mL. Under these conditions, daptomycin passes through the filter but pyrogens such as lipopolysaccharides (LPS) do not.
  • the pH of the filtrate is lowered to pH 2.5 to 4.5 and the filtrate is concentrated on a 10,000 MWCO ultra-filter to approximately 120 mg/mL. Under these conditions, daptomycin is retained on the filter.
  • the pH of the filtrate is pH 3.5. Subsequent to concentration, the concentration of daptomycin is adjusted to 105 mg/mL, checked for endotoxin levels, and used to fill vials under aseptic conditions.
  • reverse osmosis nanofiltration is performed at pH 1.5-3.0.
  • the low pH and refrigerated conditions are used to retard degradation of purified daptomycin.
  • Daptomycin may be further filtered through a 0.2 ⁇ m filter to reduce bioburden and then lyophilized either in bulk or in vials.
  • the eluted fractions containing daptomycin are mixed with butanol (either n-, iso- or t-butanol) at a pH of approximately 4.5, in a ratio of greater than one part butanol to nine parts daptomycin solution.
  • one part butanol is mixed with four parts daptomycin solution to yield a 20% butanol solution.
  • the butanol-daptomycin solution is allowed to separate into organic and aqueous phases. Daptomycin partitions into the organic phase, which is collected.
  • daptomycin The dehydration of daptomycin in the organic solvent may stabilize daptomycin and prevent the degradation of the purified daptomycin to anhydro-daptomycin and subsequent formation of ⁇ -isomer. Finally, daptomycin can be returned to the aqueous phase by adding buffer at pH 6.5-7.5 to the organic phase. After concentration or collection of daptomycin, daptomycin is lyophilized.
  • a Salt Cloud Method (Genetic Engineering News, Vol. 19, No. 20, pages 1, 34 and 43, (November 15, 1999)] is used in the purification of daptomycin.
  • the Salt Cloud Method is a membrane-based system that combines selective separations with high-volume throughput.
  • the Salt Cloud Method can be used in conjunction with those process steps disclosed herein or separately to purify daptomycin.
  • Another embodiment of the instant invention is drawn to a chromatography method that produces the highly purified lipopeptide not dapthomycin not achievable by prior art chromatography methods.
  • the chromatography method comprises the use of modified buffer enhanced anion exchange chromatography to purify a preparation containing a lipopeptide.
  • the method is used to produce highly purified daptomycin or a daptomycin-related lipopeptide. This method, when used with partially purified daptomycin, produces daptomycin that is at least 98% pure.
  • the method also produces daptomycin that is free or essentially free ofanhydro-daptomycin.
  • the method comprises the following steps:
  • daptomycin is prepared by any method known in the art or as described herein.
  • the daptomycin preparation is then further purified by modified buffer enhanced anion exchange chromatography.
  • Daptomycin is bound to anion exchange resin in the presence of an appropriate ionic modified buffer under conditions in which daptomycin binds to the resin ion in a monomeric and non-micellar state.
  • the modified buffer comprises a buffering agent, such as, without limitation, acetate, phosphate, citrate and Tris-HCl, or any other buffering agent that buffers well at neutral pH.
  • the modified buffer further comprises one or more chaotropic agents, including, without limitation, guanidine, ammonia, urea, a strong reducing agent, benzoate, ascorbate or another ionic enhancer capable of modifying the buffer so that daptomycin is easily separated from impurities.
  • chaotropic agents including, without limitation, guanidine, ammonia, urea, a strong reducing agent, benzoate, ascorbate or another ionic enhancer capable of modifying the buffer so that daptomycin is easily separated from impurities.
  • the daptomycin-loaded resin is washed with an appropriate ionic modified buffer to elute impurities, including anhydro-daptomycin. Daptomycin is then eluted under conditions that permit the separation of daptomycin from impurities that remain bound to the resin, including the ⁇ -isomer.
  • the modified buffer is at a neutral pH (a pH of 6 to 8) and contains 2 to 6 M urea.
  • the anion exchange resin is Porous Resin P150 or Porous D50 (PE Biosystems).
  • the anion exchange resin is Porous P150.
  • daptomycin is bound to the resin in a low ionic strength buffer, washed with a low to medium ionic strength buffer and eluted with a high ionic strength buffer.
  • daptomycin is bound to the Porous P150 resin in a Tris buffer pH 7.0 containing 6 M urea.
  • the daptomycin-loaded Porous P150 resin is washed with three bed volumes of Tris buffer or other suitable buffer containing a salt level that removes contaminants and anhydro-daptomycin without eluting daptomycin. Daptomycin is eluted from the Porous P150 resin with Tris buffer or other suitable buffer under elevated salt conditions that will leave additional impurities, including a significant portion of ⁇ -isomer, bound to the column.
  • Poros P150 is used and daptomycin is bound to the resin in an acetate buffer pH 6.0 containing 2 M urea.
  • the daptomycin-loaded Poros P150 resin is washed and eluted similar to the method above except that an acetate buffer pH 6.0 containing 2 M urea is used. Product fractionation may be measured by HPLC or by UV monitoring.
  • the modified buffer enhanced anion exchange chromatography may be performed by column chromatography or may be accomplished in batch mode. Radial flow chromatography may also be used, as described in United States Patents 5,756,680, 4,865,729, 4,840,730 or 4,708,782.
  • the modified buffer enhanced anion exchange resin may be washed and eluted with stepwise salt gradients or with a continuous salt gradient.
  • a suitable stepwise or continuous salt gradient is any one that permits the separation of daptomycin from impurities including, but not limited to, anhydro-daptomycin and ⁇ -isomer.
  • a continuous salt gradient is 0 to 1000 mM NaCl.
  • the salt gradient is 100 to 500 mM NaCl or 0 to 400 mM NaCl.
  • a novel combination of process chromatography steps is used to purify daptomycin or a daptomycin-related lipopeptide.
  • the method comprises anion exchange chromatography, small particle reverse phase chromatography and modified buffer enhanced anion exchange chromatography.
  • the purification method may further comprise altering the fermentation conditions in which the A21978C-containing crude product is produced by Streptomyces roseosporus. These methods produce daptomycin or a daptomycin-related lipopeptide that is at least 98% pure. In a preferred embodiment, the methods produce daptomycin or a daptomycin-related lipopeptide that is more than 99% pure.
  • the organic solvent in the daptomycin preparation is reduced by any method known in the art.
  • the organic solvent is reduced by anion exchange chromatography, as described supra.
  • Daptomycin should be eluted from the column in a buffer compatible with the buffer required for the modified buffer enhanced chromatography.
  • the elution buffer may be exchanged for the modified buffer by reverse osmosis or filtration on a 10,000 MWCO filter.
  • the organic solvent is reduced by evaporation or dilution in buffer.
  • the reverse phase chromatography solvent and residual salt is removed using reverse osmosis at pH 1.5-4.0 or ultrafiltration at pH 2.5-4.5.
  • the resultant product may be frozen for bulk storage or dried by lyophilization and then rehydrated in water or in the buffer used for the modified buffer enhanced anion exchange chromatography.
  • Daptomycin is further purified by modified buffer enhanced anion exchange chromatography as described supra.
  • the purified daptomycin is filtered and concentrated under refrigerated conditions. Filtering daptomycin may be performed by any method known in the art. In a preferred embodiment, daptomycin is depyrogenated and concentrated as described supra. Alternatively, daptomycin may be concentrated by reverse osmosis under refrigerated conditions at a pH of 1.5 to 4. The low pH and refrigerated conditions are used to retard the degradation of purified daptomycin.
  • the eluted fractions containing daptomycin from the modified buffer enhanced anion exchange chromatography may be mixed with butanol (either n-, iso- or t -butanol) at a pH of approximately 4.5, in a ratio of greater than one part butanol to nine parts daptomycin solution.
  • one part butanol is mixed with four parts daptomycin solution to yield a 20% butanol solution.
  • the butanol-daptomycin solution is allowed to separate into organic and aqueous phases. Daptomycin partitions into the organic phase, which is collected.
  • the dehydration of daptomycin in the organic solvent may stabilize daptomycin and prevent the degradation of the purified daptomycin to anhydro-daptomycin and subsequent formation of ⁇ -isomer.
  • daptomycin After concentration or collection of daptomycin, daptomycin is lyophilized.
  • the process chromatography is used to purify lipopeptides other than daptomycin, such as those described supra.
  • the lipopeptide is a daptomycin-related molecule, including, inter alia, daptomycin, A54145, a daptomycin-related lipopeptide disclosed in United States Patent 4,537,717, 4,482,487, Re. 32,311, Re. 32,310, 5,912,226, currently in reissue as United States Serial No. 09/547,357, United States Provisional Applications Nos. 60/170,943, 601170,946 or 60/170,945, filed December 15, 1999, United States Provisional Application No.
  • n-decanoyl side chain of daptomycin is replaced by an n-octanoyl, n-nonanoyl, n-undecanoyl, n-dodecanoyl, -tridecanoyl or n-tetradecanoyl side chain.
  • the lipopeptide is daptomycin.
  • Micelles are aggregates of amphipathic molecules. In aqueous media, the lipophilic parts of the molecules are oriented toward the interior of the micelle and the hydrophilic parts of the molecules are in contact with the aqueous media. Micelles form spontaneously in a solution containing amphipathic molecules if the concentration of the molecules is high enough.
  • Micelle formation causes changes in several bulk physical properties of a solution including changes in osmotic pressure, turbidity, electrical conductance, surface tension, co-ion and counterion activities (in the case of ionic amphipathic molecules), refractive index, UV and NMR spectra, partial molar volume, viscosity, diffusion coefficient and dye solubilization.
  • the cmc can be determined by measuring one or more of these micelle-dependent physical properties as a function of concentration of the amphipathic molecule.
  • the size and shape of micelles can be determined by dynamic laser light scattering, ultracentrifugation, viscosity and/or low-angle X-ray scattering experiments. Micelles can also exist in liquid crystal phases.
  • Lipopeptides may be aggregated into micelles by providing a concentration of lipopeptide that is greater than the cmc of the lipopeptide.
  • the cmc is dependent upon the nature of the lipopeptide and the temperature, salt concentration and pH of the aqueous solution comprising the lipopeptide. With respect to the nature of the lipopeptide, the cmc of a lipopeptide is reduced by the addition of CH 2 groups to the lipophilic carbon chains.
  • an A-21978 type antibiotic in which the n-decanoyl fatty acid side chain is replaced by n-octanoyl, or -nonanoyl fatty acid side chain will have a higher cmc
  • an A-21978 antibiotic in which the n-decanoyl fatty acid side chain of daptomycin is replaced by an n-undecanoyl, n-dodecanoyl, -tridecanoyl or n-tetradecanoyl fatty acid side chain will have a lower cmc relative to daptomycin.
  • the cmc of a lipopeptide may be manipulated by adding or subtracting a CH 2 group to the lipopeptide.
  • the lipopeptide is A-21978, in which the n-decanoyl fatty acid side chain of daptomycin is replaced by an n-octanoyl, n-nonanoyl, n-undecanoyl, -dodecanoyl, n-tridecanoyl or n-tetradecanoyl fatty acid side chain.
  • cmc for a lipopeptide such as daptomycin Given the cmc for a lipopeptide such as daptomycin, one may calculate the approximate cmc of a related lipopeptide in which the n-decanoyl fatty acid side chain is replaced by an n-octanoyl, n-nonanoyl, n-undecanoyl, n-dodecanoyl, n-tridecanoyl or n-tetradecanoyl fatty acid side chain. The above may be carried out by methods known by one skilled in the art.
  • cmc for one lipopeptide one can calculate the approximate cmc for a lipopeptide that contains a related peptide moiety.
  • cmc for daptomycin and the teachings of the prior art, one may readily determine the cmc for a related lipopeptide such as A54145, a daptomycin-related lipopeptide disclosed in United States Patent 4,537,717, 4,482,487, Re. 32,311, Re. 32,310, 5,912,226, currently in reissue as United States Serial No. 09/547,357, United States Provisional Applications Nos. 60/170,943, 60/170,946 or 60/170,945, filed December 15, 1999, United States Provisional Application No. 60/208,222, filed May 30, 2000.
  • the cmc of a lipopeptide is manipulated by changing the temperature of the solution comprising the lipopeptide.
  • the cmc for a lipopeptide usually increases with increasing temperature of the solution.
  • micelle formation is promoted by decreasing the temperature and is hindered by increasing the temperature.
  • a solution comprising a lipopeptide may form micelles at 4°C because at that temperature the cmc is lowered and the lipopeptide concentration is above the cmc; however, the same lipopeptide solution may be monomeric at 20°C because the cmc has increased with the temperature and the lipopeptide concentration is now below the cmc.
  • the concentration of a lipopeptide is higher than the cmc at one temperature and is lower than the cmc at another, higher temperature.
  • the lipopeptide is daptomycin or a daptomycin-related molecule, such as those described supra. In an even more preferred embodiment, the lipopeptide is daptomycin.
  • the ability to manipulate the formation of micelles of a lipopeptide by using different temperatures to affect the cmc is used in the purification of the lipopeptide.
  • the lipopeptide is daptomycin or a related molecule, such as those described supra.
  • the lipopeptide is daptomycin.
  • the ability to manipulate lipopeptide micelle formation by altering the temperature is used to make pharmaceutical compositions that are micellar under certain temperature conditions and monomeric under other temperature conditions.
  • the pharmaceutical compositions comprise daptomycin or a daptomycin-related lipopeptide, as described supra.
  • the pharmaceutical compositions comprise daptomycin.
  • an electrolyte is used to decrease the cmc of an ionic lipopeptide.
  • a salt such as NaCl
  • the lipopeptide is daptomycin or a daptomycin-related molecule, such as that described supra.
  • the peptide moiety of daptomycin contains three aspartic acid residues and an L-threo-3-methylglutamic acid residues (3-MG), all of which would be charged at neutral pH.
  • the salt concentration is at least 100 mM. In a more preferred embodiment, the salt concentration is 150 mM to 300 mM salt. In an even more preferred embodiment, the salt is NaCl.
  • a decrease in the cmc is also observed with addition of an electrolyte for other lipopeptides, such as molecules related to daptomycin that contain aspartic acid residues, 3-MG residues or other charged residues. Therefore, in a preferred embodiment, a salt is added to a solution to decrease the cmc of a daptomycin-related lipopeptide, such as A54145, a daptomycin-related lipopeptide disclosed in United States Patent 4,537,717, 4,482,487, Re. 32,311, Re. 32,310, 5,912,226, currently in reissue as United States Serial No. 09/547,357, United States Provisional Applications Nos.
  • a daptomycin-related lipopeptide such as A54145, a daptomycin-related lipopeptide disclosed in United States Patent 4,537,717, 4,482,487, Re. 32,311, Re. 32,310, 5,912,226, currently in reissue as United States Serial No. 09/547,357, United
  • the salt concentration is decreased in order to increase the cmc of an ionic lipopeptide.
  • the ionic lipopeptide is daptomycin or a daptomycin-related lipopeptide, as described supra.
  • the ability to manipulate the formation of micelles of a lipopeptide by altering electrolyte concentration to affect the cmc is used in the purification of the lipopeptide.
  • the lipopeptide is daptomycin or a daptomycin-related molecule, such as those described supra.
  • the lipopeptide is daptomycin.
  • the ability to manipulate lipopeptide micelle formation by electrolyte concentration is used to make pharmaceutical compositions that are micellar at certain electrolyte concentrations and monomeric under other electrolyte concentrations.
  • the pharmaceutical compositions comprise daptomycin or a daptomycin-related lipopeptide, as described supra.
  • the pharmaceutical compositions comprise daptomycin.
  • the pH of a solution comprising a lipopeptide is manipulated to influence the cmc of the lipopeptide.
  • the lipopeptide is daptomycin or a daptomycin-related molecule, such as those described supra.
  • the lipopeptide is daptomycin.
  • the pH is manipulated so that the concentration of a lipopeptide is higher than the cmc at one pH and is lower than the cmc at another pH. For instance, for daptomycin, the cmc at pH 4.0 in water at a temperature of 20-25°C was much lower than at pH 6.0 or 7.5. At pH 4.0, the cmc is approximately 400 ⁇ g/mL under these conditions. See Fig.
  • daptomycin is monomeric even at 150 mg/mL daptomycin at pH 6.5 (wherein the salt concentration is 150 mM to 300 mM NaCl and the temperature is 4°C).
  • the cmc at pH 4.0 is lower than in solutions of either higher pH or lower pH.
  • the change in cmc at different pH levels may also be used for other charged lipopeptides, including lipopeptides that are related to daptomycin, as described supra.
  • the ability to manipulate the formation of micelles of a lipopeptide by altering the pH to affect the cmc is used in the purification of the lipopeptide.
  • the lipopeptide is daptomycin or a daptomycin-related molecule, such as those described supra.
  • the lipopeptide is daptomycin.
  • the ability to manipulate lipopeptide micelle formation by pH is used to make pharmaceutical compositions that are micellar at a particular pH and monomeric under another pH.
  • the pharmaceutical compositions comprise daptomycin or a daptomycin-related lipopeptide, as described supra.
  • the pharmaceutical compositions comprise daptomycin.
  • the lipopeptide may be part of a mixed micelle.
  • a mixed micelle is one in which the lipopeptide forms a micelle with one or more other types of amphipathic molecules.
  • amphipathic molecules include, without limitation, medium and long chain fatty acids, phosphoglycerides (phospholipids), sphingomyelin, glycolipids and cholesterol.
  • medium chain-length alcohols can be incorporated into the micelle, where they reduce electrostatic repulsion and steric hindrance, thus lowering the cmc of the lipopepride.
  • the addition of one or more types of amphipathic molecules can be used to alter the structure of the micelle from a spherical micelle (See Fig.
  • mixed micelles comprising phospholipids and/or glycolipids will cause a spherical micelle to convert to a lipid bilayer structure, which serve as permeability barriers to ions and most polar molecules.
  • the mixed micelle can be formed from two or more different lipopeptides.
  • the mixed micelle can be formed from daptomycin and another lipopeptide, such as A54145 or a daptomycin-related lipopeptide, as discussed supra.
  • the mixed micelle may comprise a lipopeptide along with one or more therapeutically useful amphipathic molecules, such as an antibiotic, an anti-inflammatory or an anti-fungal agent, which are known to those having ordinary skill in the art.
  • the lipopeptide is daptomycin or a daptomycin-related lipopeptide such as A5414S, the daptomycin-related lipopeptides disclosed supra, or an A-21978 antibiotic in which the n-decanoyl fatty acid side chain of daptomycin is replaced by an n-octanoyl, n-nonanoyl, n-undecanoyl, n-dodecanoyl, n-tridecanoyl or n-tetradecanoyl fatty acid side chain.
  • the lipopeptide is daptomycin.
  • the micelle whether mixed or comprising a single type of lipopeptide molecule, comprises a lipopeptide that is therapeutically useful.
  • the lipopeptide is an antibiotic.
  • the lipopeptide is daptomycin. Daptomycin forms micelles of approximately 5.4 nm (54 ⁇ ) at a concentration of 1 mg/mL at pH of approximately 4.0 in water. See Fig. 16.
  • the micelles comprise one or more different types of therapeutic substances.
  • a therapeutic substance can be mixed with the lipopeptide in solution such that a micelle is formed from the lipopeptide and the therapeutic substance is trapped in the hydrophobic interior.
  • a therapeutic substance is mixed with a lipopeptide and one or more other amphipathic molecules such that a mixed micelle is formed from the lipopeptide and other amphipathic molecules and the therapeutic substance is found in the hydrophobic interior.
  • the therapeutic substance is an antibiotic, an anti-inflammatory or an anti-fungal agent.
  • the therapeutic substance is an antibiotic or antifungal agent disclosed infra.
  • the therapeutic substance is soluble in a hydrophobic environment but is not soluble in an aqueous solution.
  • the lipopeptides may be formed into liposomes, which are vesicular micelles in which a spherical lipid bilayer surrounds an aqueous interior. See Fig. 14, part c. Liposomes are advantageous for therapeutic uses because they easily fuse with a plasma membrane and can also be used to trap substances in their inner aqueous compartment.
  • the substance can be one that is only soluble in aqueous solutions.
  • a solution comprising a lipopeptide and another amphipathic molecule can be sonicated to produce liposomes.
  • the lipopeptide alone can be sonicated to produce liposomes.
  • the liposome comprises daptomycin or a daptomycin-related lipopeptide such as A54145, a lipopeptide disclosed in United States Patent 4,537,717, 4,482,487, Re. 32,311, Re. 32,310, 5,912,226, currently in reissue as United States Serial No. 09/547,357, United States Provisional Applications Nos. 60/170,943, 60/170,946 or 60/170,945, filed December 15, 1999, United States Provisional Application No.
  • n-decanoyl fatty acid side chain of daptomycin is replaced by an n-octanoyl, n-nonanoyl, n-undecanoyl, -dodecanoyl, n-tridecanoyl or n-tetradecanoyl fatty acid side chain.
  • the lipopeptide is daptomycin.
  • the liposomes comprise one or more therapeutic substances in their inner aqueous compartments.
  • the therapeutic substance is an antibiotic, an anti-inflammatory or an anti-fungal agent.
  • the therapeutic substance is an antibiotic or antifungal agent disclosed infra.
  • the therapeutic substance is soluble in aqueous solution.
  • a pharmaceutical composition comprises the liposome.
  • a pharmaceutical composition comprises lipopeptide micellar-type arrangements containing a therapeutic substance.
  • the lipopeptide micellar-type arrangements may be spherical micelles, mixed micelles or liposomes.
  • Pharmaceutical compositions comprising lipopeptide micelles may minimize local irritation upon injection or when administered intravenously, in one embodiment, the pharmaceutical composition comprises a salt, a buffer to maintain a particular pH and micelles.
  • the pharmaceutical composition comprises one or more agents to stabilize the micelles and/or to stabilize the lipopeptide or other therapeutic substance.
  • the pharmaceutical composition also comprises one or more therapeutic substances.
  • the therapeutic substance is an antibiotic, an anti-inflammatory or an antifungal agent.
  • the therapeutic substance is an antibiotic or antifungal agent disclosed infra.
  • the therapeutic substance can be in addition to the therapeutic substance that is incorporated into the micelle, or can be the therapeutic agent that is incorporated into the micelle.
  • the pharmaceutical composition can be dried or lyophilized, in which case the micelles are formed when either an aqueous solution, such as water or a buffer is added to the pharmaceutical composition.
  • the pharmaceutical composition is lyophilized and contains a physiological concentration of salt when reconstituted and a buffer that maintains a pH at which micelles spontaneously form at room temperature when sterile water or other buffer is added.
  • the pharmaceutical composition comprises daptomycin or related lipopeptide, such as A54145, the daptomycin-related lipopeptides disclosed supra, or an A-21978 antibiotic in which the n-decanoyl fatty acid side chain of daptomycin is replaced by an n-octanoyl, n-nonanoyl, n-undecanoyl, n-dodecanoyl, n-tridecanoyl or n-tetradecanoyl fatty acid side chain.
  • the lipopeptide is daptomycin.
  • the pharmaceutical composition is aqueous. This is preferred when liposomes are used.
  • the pharmaceutical composition comprises a stabilizing agent for the liposomes.
  • the micellar solution is isolated and/or purified.
  • micelles are isolated from smaller substituents by ultrafiltration. The choice of ultrafiltration membrane will be based upon the size of the micelle. In general, a 10,000 NMW or 30,000 NMW membrane will be sufficient to retain micelles while permitting smaller substituents, such as contaminants to flow through.
  • micelles can be isolated and/or purified by dialysis, density gradient centrifugation or size exclusion chromatography. These methods are well-known in the art. In one embodiment, the micelles are more than 30% pure, where purity is measured as the weight of the micelles compared to the weight of monomeric forms of the lipopeptide or of other molecules. In a preferred embodiment, the micelles are more than 50%, 60%, 70%, 80%, 90% or 95% pure.
  • the ability to form lipopeptide micelles and then to disassociate them by altering temperature, pH, electrolyte concentration and/or lipopeptide concentration provides a method for purifying lipopeptides.
  • the method comprises purifying lipopeptides from low molecular weight contaminants by subjecting lipopeptides to conditions in which the lipopeptides form micelles and then separating the micelles from the contaminants by a size selection technique, such as ultrafiltration or size exclusion chromatography.
  • the method comprises concentrating lipopeptides by subjecting lipopeptides to conditions in which the lipopeptides form micelles and then concentrating them by a size selection technique.
  • the method comprises both purification and concentration as a single step.
  • the method comprises purifying a lipopeptide from high molecular weight contaminants, including pyrogens (e.g., lipopolysaccharide), by subjecting the lipopeptide to conditions under which the lipopeptide is monomeric and then separating the monomeric lipopeptide solution from the high molecular weight contaminants by a size separation technique.
  • the size separation technique is ultrafiltration, as discussed supra.
  • the lipopeptide is daptomycin or related lipopeptide, such as A54145, the daptomycin-related lipopeptides disclosed supra , or an A-21978 antibiotic in which the n-decanoyl fatty acid side chain of daptomycin is replaced by an n-octanoyl, n-nonanoyl, n-undecanoyl, n-dodecanoyl, n-tridecanoyl or n-tetradecanoyl fatty acid side chain.
  • the lipopeptide is daptomycin.
  • the clarified preparation is then applied to an anion exchange resin, such as FP-DA 13, as described supra.
  • Daptomycin is eluted from the column with one to three column volumes of an elevated salt buffer containing 300 to 500 mM NaCl.
  • the eluted daptomycin preparation is adjusted to a pH of 2.5 to 5.0 using an acid.
  • the acid is dilute phosphoric acid.
  • the daptomycin forms a micelle.
  • the daptomycin preparation is filtered on a 10,000 to 30,000 NMW ultrafiltration membrane. During ultrafiltration, the daptomycin preparation is washed with a buffer containing 30 mM sodium acetate pH 3.5 and at temperatures of up to 15°C. The initial salt concentration is 30b mM NaCl due to the elution conditions, but the salt concentration decreases as washing continues. Because daptomycin is in micellar form, it is retained on the filter while impurities smaller than the 10,000 to 30,000 (depending upon the filter used), pass through the filter. The daptomycin preparation obtained is approximately 85-90% pure.
  • the daptomycin preparation may be diluted and its pH raised to 6.5 in order to convert the daptomycin to a monomeric state.
  • the daptomycin preparation is then be passed through a 10,000 NMW ultrafiltration membrane. This optional step decreases pyrogen content significantly.
  • Another embodiment of the invention provides analytical methods for measuring the purity of daptomycin.
  • anhydro-daptomycin and the ⁇ -isomer were previously described as impurities that persistently and consistently occurred during preparation of daptomycin.
  • HPLC analyses described here an additional approximately twelve impurities produced during the production of daptomycin were distinguished, some of which had previously not been identified. These impurities were not removed after purification by the method disclosed in United States Patent 4,874,843. At least ten of these compounds have been identified (see, e.g., Figs. 2-11).
  • Any method known in the art may be used to measure the amount of other compounds in a daptomycin preparation.
  • Methods for identifying daptomycin contaminants include, without limitation, mass spectroscopy, infrared spectroscopy, capillary electrophoresis and nuclear magnetic resonance spectroscopy.
  • a preferred method for measuring the amount of other compounds in a daptomycin preparation is HPLC.
  • the first method is a slightly lower resolution method than the second method.
  • a Shimadzu or HP HPLC System with PE Nelson's Turbochrom Software Version 4.1 is used.
  • the "first" resolution method is summarized in Table 1 and the "second” resolution method is summarized in Table 2: 1.
  • Solvent Delivery System Mode Isocratic pumping Flow rate 1.5 mL/min Run time 30 minutes 2.
  • Solvent A 34% acetonitrile in 0.5% NH 4 H 2 PO 4 at pH 4.5
  • Solvent B 20% acetonitrile in 0.5% NH 4 H 2 PO 4 at pH 4.5
  • the target condition is to retain daptomycin at 15.0 ⁇ 0.5 minutes.
  • Solvent B may be used together with solvent A to adjust the HPLC mobile phase conditions to achieve the desired retention time.
  • Autosampler cooler 5 (4 to 6) °C 4. Injection volume 5 ⁇ L to 75 ⁇ L (20 ⁇ L normal) 5.
  • Detection wavelength 214 nm 8.
  • Column Temperature ambient 9. Integration A computer system or integrator capable of measuring peak area.
  • Solvent Delivery System Mode Isocratic pumping Flow rate 1.5 mL/min Run time 75 minutes 2.
  • the target condition is approximately 35% acetonitrile in 0.45% NH 4 H 2 PO 4 at pH 3.25 (50% Solvent B) to retain daptomycin at 36.0 ⁇ 1.5 minutes; however, the solvent ratio will be used to adjust the HPLC mobile phase composition to achieve the desired retention time.
  • IB-SIL Pre-column IB-SIL (Phenomenex), C-8, 5 ⁇ , 4.6 mm x 30 mm (or equivalent) 7. Detection wavelength 214 nm 8. Column Temperature 25 (22 to 28) °C 9. Integration A computer system or integrator capable of measuring peak area.
  • Another object of the instant invention is to provide purified lipopeptides, as well as salts, esters, amides, ethers and protected forms thereof, as well as pharmaceutical formulations comprising purified lipopeptides or its salts.
  • the lipopeptide is daptomycin or a daptomycin-related lipopeptide, as described supra.
  • a further object of the instant invention is to provide pharmaceutical compositions comprising lipopeptide micellar-type arrangements.
  • the lipopepetide micelles are micelles comprising daptomycin or one or more daptomycin-related lipopeptides.
  • lipopepetide micelles refers not only to all lipopepetide micellar-type arrangements, but specifically contemplates daptomycin, or related lipopeptide, such as A54145, the daptomycin-related lipopeptides disclosed supra, or an A-21978 antibiotic in which the n-decanoyl fatty acid side chain of daptomycin is replaced by an n-octanoyl, n-nonanoyl, n-undecanoyl, n-dodecanoyl, n-tridecanoyl or n-tetradecanoyl fatty acid side chain.
  • lipopeptide micellar-type arrangements specifically contemplates spherical or mixed micelles, and liposomes, as discussed supra.
  • Purified lipopeptides, pharmaceutically acceptable salts thereof, or lipopeptide micelles can be formulated for oral, intravenous, intramuscular, subcutaneous, aerosol, topical or parenteral administration for the therapeutic or prophylactic treatment of diseases, particularly bacterial infections.
  • the purified lipopeptide is purified daptomycin or a daptomycin-related lipopeptide.
  • Reference herein to "purified daptomycin,” “purified daptomycin-related lipopeptide” or “purified lipopeptide” includes pharmaceutically acceptable salts thereof.
  • Daptomycin, daptomycin-related lipopeptide or other lipopeptide micelles can be formulated using any pharmaceutically acceptable carrier or excipient that is compatible with daptomycin or with the lipopeptide of interest.
  • any pharmaceutically acceptable carrier or excipient that is compatible with daptomycin or with the lipopeptide of interest.
  • Purified daptomycin, daptomycin-related lipopeptide or other lipopeptide micelles of this invention can be mixed with conventional pharmaceutical carriers and excipients and used in the form of tablets, capsules, elixirs, suspensions, syrups, wafers, creams and the like.
  • Daptomycin, daptomycin-related lipopeptide or other lipopeptide micelles may be mixed with other therapeutic agents and antibiotics, such as discussed herein.
  • the compositions comprising a compound of this invention will contain from about 0.1 to about 90% by weight of the active compound, and more generally from about 10 to about 30%.
  • compositions of the invention can be delivered using controlled (e.g., capsules) or sustained release delivery systems (e.g., bioerodable matrices).
  • sustained release delivery systems e.g., bioerodable matrices.
  • Exemplary delayed release delivery systems for drug delivery that are suitable for administration of the compositions of the invention are described in U.S. Patent Nos. 4,452,775 (issued to Kent), 5,239,660 (issued to Leonard), 3,854,480 (issued to Zaffaroni).
  • compositions may contain common carriers and excipients, such as corn starch or gelatin, lactose, sucrose, microcrystalline cellulose, kaolin, mannitol, dicalcium phosphate, sodium chloride and alginic acid.
  • compositions may contain croscarmellose sodium, microcrystalline cellulose, corn starch, sodium starch glycolate and alginic acid.
  • Daptomycin was produced in a fermentation culture of S . roseosporus and partially purified Daptomycin (9.9 Kg) was purified by microfiltration from 5500 liters of fermentation broth by the method described in United States Patent 4,885,243. The partially purified daptomycin was further purified by the method described in US. Pat. No. 4,874,843, and resulted in a bulk daptomycin preparation with a purity of 91%. The daptomycin preparation contained fourteen impurities by HPLC analysis (see Example 8). The daptomycin preparation was applied to a Poros P150 anion exchange resin (PE Biosystems) in Tris buffer pH 7.0 containing 6M urea and allowed to bind to the resin.
  • P150 anion exchange resin PE Biosystems
  • the resin was washed with three column volumes of buffer prior to initiation of a NaCl gradient in the same buffer.
  • the contaminants can be effectively removed from the column with a fixed salt level of 30 mM NaCl.
  • the elution of purified daptomycin from the resin occurred at approximately 300 mM NaCl during a 0 to 1000 mM NaCl gradient. Daptomycin eluted from the column was greater than 99 % pure as measured by the "first" HPLC method.
  • the purified daptomycin contained only one detectable daptomycin contaminant. Anhydro-daptomycin and ⁇ -isomer were undetectable (less than 0.01% contamination). The level of the unidentified contaminant was greater than 0.1% and less than 0.5%.
  • a bulk daptomycin preparation with a purity of 91% was prepared as described in Example 1.
  • the product was applied to a Poros D50 anion exchange resin (PE Biosystems) in an acetate buffer pH 7.0 containing 6M urea.
  • the Poros D50 resin was washed and eluted in the same manner as described in Example 1.
  • Daptomycin eluted from the column was 96.92 % pure as measured by the "second" HPLC method.
  • the product of this invention contained only two of the initial fourteen impurities (less than 0.5% contamination). Anhydro-daptomycin could not be detected in the purified daptomycin preparation (less than 0.01 % contamination and with precise quantitation at less than 0.05%).
  • a fermentation broth containing daptomycin was produced as described in Example 1.
  • the fermentation broth was clarified by microfiltration.
  • the clarified product was extracted with 20% n-butanol or iso-butanol at pH 4.5 (one part butanol to four parts clarified solution). Re-extraction of the clarified solution was performed to achieve a yield of partially purified daptomycin of greater than 90% of the total daptomycin in the clarified solution.
  • Daptomycin was recovered from the butanol phase by the addition of a pH 6.5 aqueous buffer in a volume that is one-half or more of the volume of butanol to extract daptomycin from the butanol phase into the aqueous phase.
  • the butanol extraction step resulted in a partially purified daptomycin preparation that was purified 5-fold and concentrated 10-fold relative to the clarified solution.
  • aqueous daptomycin preparation was then purified by the method disclosed in US. Pat. No. 4,874,843, resulting in daptomycin that was 91% pure. Daptomycin contained fourteen impurities.
  • the product was applied to a Poros D50 resin in a Tris buffer at pH 7.0 containing 6M urea. The resin was washed with three bed volumes of Tris buffer at pH 7.0 containing 6M urea prior to initiation of a NaCl gradient from 0 to 1000 mM in the same buffer. Elution of purified daptomycin from the resin occurred at approximately 300 mM NaCl. Daptomycin was 98% pure as measured by the "second" HPLC method.
  • Daptomycin is fermented as described in Example 1.
  • the 5500 liters fermentation broth contains 13 Kg daptomycin.
  • the fermentation broth is directly extracted with 20% n-butanol at pH 4.5, which partitions daptomycin into the butanol. Re-extractions of the fermentation broth with butanol are performed to achieve a yield of greater than 90% of the total daptomycin in the fermentation broth.
  • the butanol phase is extracted with an aqueous acetate buffer at pH 6.5, resulting in daptomycin that is purified 5-fold (35%) and concentrated to-fold relative to the fermentation broth
  • the aqueous daptomycin is microfiltered by the method described in United States Patent 4,885,243, then purified by the method of US. Pat. No.
  • a daptomycin preparation with a purity of 93% was prepared as described in Example 1.
  • the product was applied to a Poros P150 resin (PE Biosystems) in an acetate buffer pH 6.0 containing 2M urea.
  • the Poros P150 resin was washed with three column volumes of the buffer.
  • Daptomycin was eluted from the resin using a 0 to 400 mM NaCl gradient in the acetate buffer pH 6.0 containing 2M urea. Daptomycin eluted between 150 and 300 mM NaCl. Daptomycin eluted from the column was 99.0 to 99.5 % pure as measured by the "first" HPLC method.
  • Daptomycin contained trace amounts of four impurities that were less than 1% of the total of daptomycin. Anhydro-daptomycin could not be detected in the purified daptomycin preparation (less than 0.02% contamination).
  • a daptomycin preparation with a purity of 93% was prepared as described in Example 1.
  • the product was applied to a Poros P150 resin (PE Biosystems) in an acetate buffer pH 6.0 containing 2M urea.
  • the column was washed with six column volumes of 60 mM NaCl in acetate buffer pH 6.0 containing 2,M urea (the "wash buffer”).
  • the wash buffer may vary from 50-75 mM NaCl.
  • the wash removes virtually all anhydro-daptomycin.
  • Daptomycin is eluted with sixteen column volumes of 250 mM NaCl in acetate buffer pH 6.0 containing 2M urea. Daptomycin is 98.5 to 99.5% pure as measured by the "first" HPLC method.
  • a daptomycin preparation as described in Example 1 was prepared using a method that significantly reduced the concentration of solvent required to perform the HP-20ss chromatography.
  • the solvent for elution of daptomycin 40% acetonitrile or 55-60% isopropyl alcohol, was reduced to 12% and 25%, respectively, when HP-20ss chromatography was conducted at neutral pH rather than acidic pH as described in United States Patent 4,874,843.
  • pH shifts can be used to recycle the HP-20ss resin without solvent removal.
  • daptomycin is loaded on an equilibrated HP-20ss column, such as one that has been equilibrated in 60 mM acetate, pH 6.6.
  • the column is washed with five to eight column bed volumes (CBV) wash buffer.
  • An exemplary wash buffer is 5% isopropyl alcohol/60mM acetate, pH 6.6.
  • Daptomycin is eluted from the column with elution buffer.
  • An exemplary elution buffer is two to three CBV 25% isopropyl alcohol/60 mM acetate pH 6.6.
  • the column is stripped with strip buffer.
  • the column is stripped with one CBV 40% isopropyl alcohol/60 mM acetate pH 6.6-7.0.
  • the daptomycin solution is adjusted to pH 3.5-4.0 and is reloaded on to the HP-20ss column in order to further enhance purity.
  • the daptomycin eluted from the HP-20ss column at pH 6.5 is adjusted to pH 3.5 using 0.25M phosphoric acid.
  • the daptomycin solution is reloaded on the previously stripped HP-20ss column that has been equilibrated in 60 mM acetate, pH 3.5.
  • the column is washed with a pH adjusting buffer such that the pH is 6.5.
  • An exemplary pH adjusting buffer is five to eight CBV 5% isopropyl alcohol/60 mM acetate, pH 6.6.
  • the daptomycin is eluted with elution buffer and may be further purified by anion exchange or other purification methods, if desired.
  • the HP-20ss column is stripped with strip buffer and cleaned prior to reuse.
  • An exemplary cleaning process includes washing with three CBV 0.5M NaOH, washing with one CBV water, and then washing with 0.25M phosphoric acid prior to equilibration.
  • the column may be stored in 0.5M NaOH.
  • Bulk daptomycin prepared as described in Example 1 was characterized via semi-preparative HPLC and characterized by liquid chromatography/mass spectroscopy (LC/MS) using both positive and negative ion modes.
  • LC/MS liquid chromatography/mass spectroscopy
  • An impurity profile of the bulk daptomycin prior to chromatography on the Poros P 150 anion exchange resin is shown in Table 3 and a chromatogram of the bulk daptomycin preparation is shown in Fig. 12.
  • the bulk daptomycin may be purified on Poros P150 as described above in Examples 1 or 5-6 or may be purified on Poros D50 as described above in Examples 2-4.
  • a chromatogram shows that daptomycin purity is greater than 99.0%, with ⁇ -isomer and anhydro-daptomycin below the level of detection (less than 0.05% of total).
  • a fermentation culture of S . roseosporus NRRL Strain 15998 is conducted in a controlled decanoic acid feed fermentation at levels that optimize the production of the antibiotic while minimizing the production of contaminants.
  • the residual decanoic acid feed is measured by gas chromatography and the target residual level is 10 ppm decanoic acid from the start of induction (approximately at hour 30) until harvest.
  • Centrifugation of the culture and subsequent analysis of the clarified broth are used to measure the production of daptomycin by HPLC.
  • the harvest titer is typically between 1.0 and 3.0 grams per liter of fermentation broth.
  • the fermentation is harvested either by microfiltration using a Pall-Sep or by full commercial-scale centrifugation and depth filter.
  • the clarified broth is applied to an anion exchange resin, Mitsubishi FP-DA 13, washed with 30 mM NaCl at pH 6.5 and eluted with 300 mM NaCl at pH 6.0-6.5.
  • the FP-DA 13 column is washed with 60 mM NaCl at pH 6.5 and eluted with 500 mM NaCl at pH 6.0-6.5.
  • the pH is adjusted to 3.0 to 4.8 and the temperature is adjusted to 2-15°C. Under these conditions, daptomycin forms a micelle.
  • micellar daptomycin solution is purified by washing the micellar preparation while it is retained on a ultrafilter using a 10,000 NMW filter (AG Technology Corp. UF hollow fiber or equivalent) in any configuration.
  • the daptomycin micelles are retained by the filter, but a large number of impurities are eliminated because they pass through the 10,000 NMW fitter Ultrafiltration of daptomycin micelles increases daptomycin purity from approximately 40% to 80% or greater.
  • the eluate is applied to a HIC resin, HP-20ss, washed with 30% acetonitrile, and eluted with 35% acetonitrile at pH 4.0-5.0.
  • the HIC resin is washed with 20-30% isopropyl alcohol and eluted with 30-40% isopropyl alcohol at pH 3.5-6.5. Under these conditions of increased solvent and a higher pH of 6.0-7.5, daptomycin reverts to a single, non-micelle state.
  • the eluate is applied to FP-DA 13 resin column and washed and eluted as before.
  • the final anion exchange step reduces solvent by one third or more.
  • Reverse osmosis diafiltration and concentration at pH 1.5-2.5 is performed using an 0.2 ⁇ m filter and the daptomycin preparation is frozen.
  • a final reverse osmosis diafiltration is conducted with Water-For-Injection (WFI) to wash daptomycin and adjust its concentration prior to sterile-filling. Vials or bulk quantities of daptomycin are then lyophilized.
  • WFI Water-For-Injection
  • Lyophilized daptomycin purified as described in any of the above-described examples, such as that described in Example 9 is reconstituted in physiologic saline (approximately 140 mM NACl) at a pH of 4.0-5.0. Under these conditions, daptomycin is present as a micelle, and can be used for injection or intravenous, parenteral, oral or topical administration.
  • Daptomycin is produced by fermentation and clarified from the broth by microfiltration as described in Example 9.
  • the clarified broth is applied to an anion exchange resin, Mitsubishi FP-DA 13, washed with 30 mM NaCl at pH 6.5 and eluted with 300 mM NaCl at pH 6.0-6.5 to give a daptomycin preparation that is approximately 40% pure.
  • the eluate is adjusted to pH 3.5 with dilute phosphoric acid such that virtually all of the daptomycin forms micelles.
  • the micelle preparation is loaded on a 10,000 NMW ultrafiltration membrane.
  • the daptomycin preparation is washed with 30 mM sodium acetate pH 3.5 and at temperatures of up to 15°C. The reduction in volume and washing lowers the contamination level, which results in an 85% pure daptomycin preparation.
  • the daptomycin preparation can be further purified using any of the methods described herein.
  • Daptomycin is produced by fermentation, clarified from the broth by microfiltration, and fractionated on the FP-DA 13 resin as described in Example 9. The eluate is adjusted to pH 3.5 with dilute phosphoric acid such that virtually all of the daptomycin forms micelles. The micelle preparation is loaded on a 10,000 NMW ultrafiltration membrane. The daptomycin preparation is washed with 30 mM sodium acetate pH 3.5 and at temperatures of up to 15°C. The reduction in volume and washing lowers the contamination level, which results in an 80-90% pure daptomycin preparation. The daptomycin preparation can be further purified using any of the methods described herein.
  • Daptomycin is produced by fermentation and clarified from the broth using microfiltration as described in Example 9.
  • the preparation is purified using hydrophobic interaction chromatography, as described in United States Patent 4,874,843, herein incorporated by reference: In this method, repeated column chromatography on HP-20 and HP-20ss resin is used. Daptomycin purity is 93% with visible impurities on HPLC chromatographs and measurable pyrogen.
  • the product is diluted in water and its pH was adjusted to pH 6.5 with NaOH or the equivalent.
  • the daptomycin preparation is filtered through a 10,000 NMW ultrafiltration membrane. Under these conditions, daptomycin is monomeric and passes through the ultrafiltration membrane. The resulting product remains 93% pure, but several impurities that had been present at 0.1-0.2% are removed by the ultrafiltration membrane. In addition, pyrogen content is reduced to undetectable levels.
  • a daptomycin preparation of approximately 93% purity is prepared as described in Example 13.
  • the daptomycin preparation is converted to a micellar state by lowering the pH to 4.7 with HCl or equivalent and chilling the daptomycin preparation to 2-5°C.
  • the product is concentrated from 400 liters to three liters and to a final concentration of approximately 100 mg/ml by filtration on a 10,000 NMW ultrafiltration membrane. Under these conditions, daptomycin is retained by the membrane. This results in a large increase in daptomycin concentration.
  • the purity is approximately 93%.
  • a daptomycin preparation is prepared as described in Example 14. Vials are filled with approximately 250 mg daptomycin and lyophilized. The daptomycin is reconstituted in 50 ml of sterile 150 mM saline at a pH of 4.0-5.0 for administration to a human or animal patient. The dose of daptomycin that is administered will depend upon the nature of the infection, the age and weight of the patient, and the species of animal. At a pH of 4.0-5.0 in 150 mM saline, the daptomycin will be present in a micellar state, which is soluble and suitable for intravenous, intramuscular or parenteral injection. The formulation will minimize any local irritation due to the lipopeptide nature of daptomycin.
  • Daptomycin micelles were produced using daptomycin at a concentration of 1.0 mg/mL in water at pH 4.0 at 25°C.
  • the size of a daptomycin micelle was measured using a ZetasizerTM (Malvern Instruments, Model 3000 HS). The count rate of 36.3, the cell type was a capillary cell, the detection angle (deg) was 90°, and the wavelength (nm) was 633. Results indicated that the diameter of the micelle was 54 ⁇ , which is about twice the diameter of a single monomeric daptomycin molecule. See Fig. 18.

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Claims (8)

  1. Procédé destiné à purifier la daptomycine, comprenant les étapes consistant à :
    a) fournir une préparation de daptomycine qui contient au moins 2,5 % d'une quantité combinée d'anhydro-daptomycine et de β-isomère de la daptomycine ;
    b) lier la préparation de daptomycine sur une résine échangeuse d'anions en présence d'un tampon modifié dans des conditions dans lesquelles la daptomycine se lie à la résine échangeuse d'anions sous une forme monomère et non-micellaire, dans lequel le tampon modifié comprend un agent tampon choisi parmi un acétate, un phosphate, un citrate et le TRIS-HCl et un ou plusieurs agents chaotropiques choisis parmi l'ammoniaque, l'urée, un benzoate et un ascorbate ;
    c) laver la résine échangeuse d'anions en présence du tampon modifié dans des conditions qui permettent l'élutlon de l'anhydro-daptomycine mais la rétention de la daptomycine ;
    d) éluer la daptomycine en présence du tampon modifié dans des conditions qui permettent de séparer la daptomycine purifiée du β-isomère de la daptomycine ; et
    e) obtenir la daptomycine purifiée.
  2. Procédé selon la revendication 1, comprenant en outre l'étape consistant à filtrer et à concentrer la daptomycine éluée.
  3. Procédé destiné à purifier la daptomycine, comprenant les étapes consistant à :
    a) laisser fermenter Streptomyces reseosporus avec une alimentation en acide n-décanoique afin de produire de la daptomycine dans un bouillon de fermentation ;
    b) clarifier le bouillon de fermentation ;
    c) soumettre le bouillon de fermentation à une chromatographie par échange d'anions afin d'obtenir une préparation enrichie en daptomycine ;
    d) soumettre la préparation enrichie en daptomycine à une chromatographie hydrophobe afin d'obtenir une préparation de daptomycine semi-purifiée ; et
    e) soumettre la préparation de daptomycine semi-purifiée à une chromatographie par échange d'anions améliorée par un tampon modifié, dans laquelle le tampon modifié comprend un agent tampon choisi parmi un acétate, un phosphate, un citrate et le TRIS-HCl et un ou plusieurs agents chaotropiques choisis parmi l'ammoniaque, l'urée, un benzoate et un ascorbate afin d'obtenir la daptomycine purifiée.
  4. Procédé selon la revendication 3, dans lequel l'alimentation en acide n-décanoïque de l'étape a) est ajustée afin d'obtenir une concentration résiduelle en acide n-décanoïque non supérieure à 50 parties par million (ppm) pendant la fermentation ;
    ladite clarification de l'étape b) comprend l'extraction du bouillon de fermentation avec un tampon comprenant du butanol ;
    la chromatographie par échange d'anions de l'étape c) est réalisée sur une résine FP-DA 13 ; ou
    l'étape c) ou l'étape e) ou les deux comprennent l'utllisation d'un gradient continu de salinité ou d'un gradient échelonné de salinité.
  5. Procédé selon la revendication 3, dans lequel la chromatographie par échange d'anions améliorée par un tampon modifié de l'étape e) comprend les étapes consistant à :
    i) fournir la préparation de daptomycine semi-purifiée issue de l'étape d) dans un tampon approprié pour une chromatographie par échange d'anions améliorée par un tampon modifié ;
    ii) lier la préparation de daptomycine sur une résine échangeuse d'anions en présence du tampon modifié dans des conditions dans lesquelles la daptomycine se lie à la résine échangeuse d'anions sous une forme monomère et non-micellaire ;
    iii) laver la résine échangeuse d'anions en présence du tampon modifié dans des conditions qui permettent l'élution de l'anhydro-daptomycine mais la rétention de la daptomycine ;
    iv) éluer la daptomycine en présence du tampon modifié dans des conditions qui permettent de séparer la daptomycine du β-isomère.
  6. Procédé selon la revendication 3, comprenant en outre :
    l'étape de chromatographie par échange d'anions avant l'étape e) ; ou
    l'étape consistant à filtrer et/ou à concentrer la daptomycine.
  7. Procédé selon la revendication 3, comprenant en outre l'étape consistant à dépyrogéner la daptomycine.
  8. Procédé selon la revendication 7, comprenant en outre l'étape consistant à lyophiliser la daptomycine.
EP01903121A 2000-01-20 2001-01-18 Lipopeptides a haute purete, micelles de lipopeptides et procedes de preparation Expired - Lifetime EP1252179B1 (fr)

Priority Applications (7)

Application Number Priority Date Filing Date Title
EP15173312.8A EP2940034B1 (fr) 2000-01-20 2001-01-18 Procédé de purification de daptomycin
EP05015374A EP1586580B1 (fr) 2000-01-20 2001-01-18 Procédé de purification de daptomycin
DK05015374.1T DK1586580T3 (da) 2000-01-20 2001-01-18 Fremgangsmåde til rensning af daptomycin
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EP2264047B1 (fr) 2015-06-24
IL226636A0 (en) 2013-06-27
JP5631439B2 (ja) 2014-11-26
DE60140631D1 (de) 2010-01-07
US20120149062A1 (en) 2012-06-14
US20050009747A1 (en) 2005-01-13
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KR20120065440A (ko) 2012-06-20
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ES2547281T3 (es) 2015-10-02
KR20070044079A (ko) 2007-04-26
CN102229650A (zh) 2011-11-02
CN101240013A (zh) 2008-08-13
CN102229650B (zh) 2014-03-12
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EP2264047A1 (fr) 2010-12-22
CA2398726A1 (fr) 2001-07-26
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PL400575A1 (pl) 2013-01-07
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IL219889A (en) 2017-01-31
US20130280760A1 (en) 2013-10-24
RU2311460C9 (ru) 2009-06-10
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US20070191280A1 (en) 2007-08-16
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